CA2493811A1 - Contact structures - Google Patents

Contact structures Download PDF

Info

Publication number
CA2493811A1
CA2493811A1 CA002493811A CA2493811A CA2493811A1 CA 2493811 A1 CA2493811 A1 CA 2493811A1 CA 002493811 A CA002493811 A CA 002493811A CA 2493811 A CA2493811 A CA 2493811A CA 2493811 A1 CA2493811 A1 CA 2493811A1
Authority
CA
Canada
Prior art keywords
disperser
combination according
wire
mesh
knit
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CA002493811A
Other languages
French (fr)
Other versions
CA2493811C (en
Inventor
Lawrence A. Smith, Jr.
Abraham P. Gelbein
John R. Adams
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Catalytic Distillation Technologies
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=31886594&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=CA2493811(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Individual filed Critical Individual
Publication of CA2493811A1 publication Critical patent/CA2493811A1/en
Application granted granted Critical
Publication of CA2493811C publication Critical patent/CA2493811C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/248Reactors comprising multiple separated flow channels
    • B01J19/2495Net-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/009Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/56Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20Organic compounds not containing metal atoms
    • C10G29/205Organic compounds not containing metal atoms by reaction with hydrocarbons added to the hydrocarbon oil
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G50/00Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002Chemical plants
    • B01J2219/00004Scale aspects
    • B01J2219/00006Large-scale industrial plants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32213Plurality of essentially parallel sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32224Sheets characterised by the orientation of the sheet
    • B01J2219/32227Vertical orientation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32224Sheets characterised by the orientation of the sheet
    • B01J2219/32231Horizontal orientation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32286Grids or lattices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32286Grids or lattices
    • B01J2219/32289Stretched materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32408Metal
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32408Metal
    • B01J2219/32416Metal fibrous
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32441Glass
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32466Composition or microstructure of the elements comprising catalytically active material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32483Plastics
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32491Woven or knitted materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/33Details relating to the packing elements in general
    • B01J2219/3306Dimensions or size aspects
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/332Details relating to the flow of the phases
    • B01J2219/3322Co-current flow

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

An internal static mixing system such as a disperser of mesh wire or expande d metal co-knit with a multi filament material selected from inert polymers, catalytic polymers, catalytic metals or mixtures in combination with a vertical reactor having a reaction zone and the disperser disposed in said reaction zone, particularly for carrying out paraffin alkylation using acid catalyst is disclosed. The wire mesh provides the structural integrity of th e system as well as the open space required in reactors for the movement of vapors and liquids though the system. The disperser may be in sheets, bundle s or bales or positioned within a frame.

Claims (26)

1. A combination of a vertical reactor for carrying out catalytic reactions comprising a vertical reactor and a disperser disposed in said vertical reactor, said disperser comprising at least 50 volume % open space.
2. The combination according to claim 1 wherein said open space is up to about 97 volume %.
3. The combination according to claim 1 wherein said disperser comprises mesh wire co-knit with a multi filament component or expanded metal intertwined with a multi filament component, said multi filament selected from inert polymers, catalytic polymers, catalytic metals or mixtures thereof.
4. The combination according to claim 3 wherein said disperser comprises a co-knit mesh of wire and polymer mesh.
5. The combination according to claim 3 wherein said disperser comprises co-knit mesh wire and fiberglass.
6. The combination according to claim 3 wherein said disperser comprises a mesh of co-knit wire and a multi filament component comprising teflon, steel wool, polypropylene, PVDF, polyester or combinations thereof.
7. The combination according to claim 3 wherein said disperser is positioned as a plurality of vertically arranged, transverse mats within and across said vertical reactor.
8. The combination according to claim 3 wherein said wire mesh provides structural integrity of the system and the open space required in reactors for the movement of vapors and liquids therethrough.
9. The combination according to claim 3 wherein said disperser comprises sheets, bundles or bales of the co-knit wire and the multi filament component or combinations thereof.
10. The combination according to claim 3 wherein said disperser comprises multi filament catalytic material of sulfonated vinyl resin, Ni, Pt, Co, Mo, Ag or mixtures thereof.
11. A combination for carrying out catalytic reactions in concurrent downflow comprising a vertical reactor, a disperser disposed in said vertical reactor, comprising at least one partially liquid reactant, catalyst and reaction conditions to maintain said partially liquid reactant at a boiling point.
12. The combination according to claim 11 wherein said disperser comprises mesh wire co-knit with a multi filament component or expanded metal intertwined with a multi filament component, said multi filament selected from inert polymers, catalytic polymers, catalytic metals or mixtures thereof.
13. The combination according to claim 11 wherein said disperser comprises a co-knit mesh of wire and polymer mesh.
14. The combination according to claim 11 wherein said disperser comprises co-knit mesh wire and fiberglass.
15. The combination according to claim 11 wherein said disperser comprises a mesh of co-knit wire and a multi filament component comprising teflon, steel wool, polypropylene, PVDF, polyester or combinations thereof.
16. The combination according to claim 11 wherein said disperser is positioned as a plurality of vertically arranged, transverse mats within and across said vertical reactor.
17. The combination according to claim 11 wherein said wire mesh provides structural integrity of the system and the open space required in reactors for the movement of vapors and liquids therethrough.
18. The combination according to claim 11 wherein said disperser comprises sheets, bundles or bales of the co-knit wire and the multi filament component or combinations thereof.
19. The combination according to claim 11 wherein said disperser comprises multi filament catalytic material of sulfonated vinyl resin, Ni, Pt, Co, Mo, Ag or mixtures thereof.
20. The combination according to claim 11 wherein at least two phases are present.
21. A disperser comprising mesh wire or expanded metal co-knit with a multi filament material selected from catalytic polymers, catalytic metals or mixtures thereof.
22. The disperser according to claim 21 wherein said disperser comprises multi filament catalytic material of sulfonated vinyl resin, Ni, Pt, Co, Mo, Ag or mixtures thereof.
23. The disperser according to claim 21 wherein said disperser comprises at least 50 volume% open space.
24. The disperser according to claim 21 wherein said disperser comprises up to about 97 volume% open space.
25. The combination according to claim 1 wherein said disperser comprises a structure that having a rigid frame made of two substantially vertical duplicate grids spaced apart and held rigid by a plurality of substantially horizontal rigid members and a plurality of substantially horizontal wire mesh tubes mounted to the grids to form a plurality of fluid pathways among the tubes, said tubes being empty or containing catalytic or non catalytic materials.
26. The combination according to claim 1 wherein said disperser comprises a structure comprising a plurality of sheets of wire mesh formed into vee shaped corrugations having flats between the vees, said plurality of sheets being of substantially uniform size having the peaks oriented in the same direction and substantially in alignment, said sheets being separated by a plurality of rigid members oriented normally to and said resting upon said vees.
CA2493811A 2002-08-15 2003-07-24 Contact structures Expired - Fee Related CA2493811C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US10/219,653 US20040052703A1 (en) 2001-08-21 2002-08-15 Contact structures
US10/219,653 2002-08-15
PCT/US2003/023132 WO2004016342A2 (en) 2002-08-15 2003-07-24 Contact structures

Publications (2)

Publication Number Publication Date
CA2493811A1 true CA2493811A1 (en) 2004-02-26
CA2493811C CA2493811C (en) 2010-07-06

Family

ID=31886594

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2493811A Expired - Fee Related CA2493811C (en) 2002-08-15 2003-07-24 Contact structures

Country Status (17)

Country Link
US (2) US20040052703A1 (en)
EP (1) EP1534406B1 (en)
JP (1) JP4700964B2 (en)
KR (1) KR100970802B1 (en)
CN (1) CN100337721C (en)
AR (1) AR040707A1 (en)
AT (1) ATE516067T1 (en)
AU (1) AU2003256743B2 (en)
BR (1) BR0313181B1 (en)
CA (1) CA2493811C (en)
EG (1) EG23477A (en)
MX (1) MXPA05001555A (en)
RO (1) RO123325B1 (en)
RU (1) RU2318590C2 (en)
TW (1) TWI288660B (en)
WO (1) WO2004016342A2 (en)
ZA (1) ZA200500098B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6858770B2 (en) * 2001-08-21 2005-02-22 Catalytic Distillation Technologies Paraffin alkylation
US20080063593A1 (en) * 2006-09-08 2008-03-13 Catalytic Distillation Technologies Low temperature process for regenerating spent sulfuric acid
CN101574632B (en) * 2008-05-09 2011-07-13 北京化工大学 Preparation method of cod-liver oil emulsion
US8235361B2 (en) * 2009-02-09 2012-08-07 Tribute Creations, Llc Structured packing for a reactor
DE102010016595B4 (en) * 2010-04-22 2012-05-31 Zeppelin Reimelt Gmbh mixer
US9551282B2 (en) * 2014-10-17 2017-01-24 General Electric Company Media pads with mist elimination features
US10967352B1 (en) 2017-04-07 2021-04-06 Triad National Security, Llc Microfluidic liquid-liquid contactor
CN108786376A (en) * 2017-04-28 2018-11-13 中国石化工程建设有限公司 A kind of method and system of recycling volatile organic matter
US11033873B2 (en) 2017-08-31 2021-06-15 Refining Technology Solutions, Llc Conversion of a hydrogen fluoride alkylation unit to a sulfuric acid alkylation unit and apparatus utilized therein

Family Cites Families (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2591343A (en) * 1949-08-10 1952-04-01 Gulf Oil Corp Tray for fractionating equipment
US2808318A (en) * 1950-09-30 1957-10-01 Little Inc A Liquid-liquid contact apparatus
US3013093A (en) * 1957-03-20 1961-12-12 Kellogg M W Co Alkylation process
NL98910C (en) * 1958-07-14
US3169835A (en) * 1959-07-01 1965-02-16 Exxon Research Engineering Co Fluidized solids technique
US3155742A (en) * 1961-09-11 1964-11-03 Shell Oil Co Alkylation process
JPS4424211Y1 (en) * 1966-12-02 1969-10-13
IL28565A (en) * 1967-08-25 1971-12-29 Hydro Chem & Mineral Corp Apparatus and process for providing direct contact between a liquid and one or more other fluids
US3585005A (en) * 1969-03-11 1971-06-15 Nat Res Dev Liquid-liquid contactor having opposing surfaces of different wetting characteristics
US4018881A (en) * 1971-07-15 1977-04-19 Exxon Research And Engineering Company High surface area alumina and method for the preparation thereof
US4057493A (en) * 1973-01-30 1977-11-08 Graham Arthur Davies Droplet control elements
JPS5237573A (en) * 1975-09-19 1977-03-23 Matsushita Electric Ind Co Ltd Catalytic treatment apparatus
US4437867A (en) * 1977-05-12 1984-03-20 Lerner Bernard J Removal of undesired components from gases
US4242530A (en) * 1978-07-27 1980-12-30 Chemical Research & Licensing Company Process for separating isobutene from C4 streams
JPS577259A (en) * 1980-06-18 1982-01-14 Japan Organo Co Ltd Catalyst used in organic reaction
US4443559A (en) * 1981-09-30 1984-04-17 Chemical Research & Licensing Company Catalytic distillation structure
US4536373A (en) * 1982-06-21 1985-08-20 Chemical Research & Licensing Company Contact structure for use in catalytic distillation
JPS5912749A (en) * 1982-07-12 1984-01-23 Kuraray Co Ltd Packing element for reaction and distillation tower
US5175135A (en) * 1987-11-23 1992-12-29 The Dow Chemical Company Alkylation of aromatic compounds to alkylates enriched in the linear substituted isomers
JPS63197533A (en) * 1987-12-28 1988-08-16 ケミカル・リサーチ・アンド・ライセンシング・カンパニー Catalytic distillation catalyst
US5204064A (en) * 1989-03-23 1993-04-20 Chemical Research & Licensing Company Apparatus for conducting a catalytic distillation process
DK168520B1 (en) 1989-12-18 1994-04-11 Topsoe Haldor As Process for liquid phase alkylation of a hydrocarbon with an olefin alkylating agent
US5266546A (en) * 1992-06-22 1993-11-30 Chemical Research & Licensing Company Catalytic distillation machine
DE59308587D1 (en) * 1993-08-26 1998-06-25 Sulzer Chemtech Ag Packing with catalytic or adsorbing agents
US5498376A (en) * 1993-11-03 1996-03-12 Lantec Products, Inc. Packing
US5431890A (en) * 1994-01-31 1995-07-11 Chemical Research & Licensing Company Catalytic distillation structure
US5446223A (en) * 1994-05-23 1995-08-29 Chemical Research & Licensing Company Alkylation of organic aromatic compounds
US5523062A (en) * 1994-11-03 1996-06-04 Chemical Research & Licening Company Catalytic distillation distribution structure
US5599997A (en) * 1995-03-14 1997-02-04 Chemical Research & Licensing Company Process for the production of cyclohexyl amine
US5730843A (en) * 1995-12-29 1998-03-24 Chemical Research & Licensing Company Catalytic distillation structure
US20020068026A1 (en) * 1997-08-08 2002-06-06 Lawrence L. Murrell Reactor
US5866736A (en) * 1997-10-14 1999-02-02 Catalytic Distillation Technologies Process for the production of alkyl benzene
US6000685A (en) * 1998-06-29 1999-12-14 Catalytic Distillation Technologies Gas/liquid contact structure
US6187980B1 (en) * 1999-09-29 2001-02-13 Catalytic Distillation Technologies Hydrogenation of benzene to cyclohexane
US6631890B1 (en) * 2000-06-30 2003-10-14 Apollo Separation Technologies, Inc Packing for column
US6858770B2 (en) * 2001-08-21 2005-02-22 Catalytic Distillation Technologies Paraffin alkylation

Also Published As

Publication number Publication date
US7850929B2 (en) 2010-12-14
EP1534406A2 (en) 2005-06-01
WO2004016342A2 (en) 2004-02-26
EP1534406B1 (en) 2011-07-13
EP1534406A4 (en) 2007-02-28
CN1658947A (en) 2005-08-24
TWI288660B (en) 2007-10-21
WO2004016342A3 (en) 2005-02-24
CN100337721C (en) 2007-09-19
AU2003256743B2 (en) 2008-06-26
RU2005107001A (en) 2005-08-10
TW200407195A (en) 2004-05-16
ATE516067T1 (en) 2011-07-15
BR0313181B1 (en) 2012-09-04
KR20050037570A (en) 2005-04-22
MXPA05001555A (en) 2005-04-19
AR040707A1 (en) 2005-04-13
EG23477A (en) 2005-11-19
JP2006500199A (en) 2006-01-05
AU2003256743A1 (en) 2004-03-03
KR100970802B1 (en) 2010-07-16
CA2493811C (en) 2010-07-06
BR0313181A (en) 2005-07-26
RU2318590C2 (en) 2008-03-10
RO123325B1 (en) 2011-08-30
ZA200500098B (en) 2005-11-30
US20060245990A1 (en) 2006-11-02
US20040052703A1 (en) 2004-03-18
JP4700964B2 (en) 2011-06-15

Similar Documents

Publication Publication Date Title
US5730843A (en) Catalytic distillation structure
Toyao et al. Heterogeneous Pt and MoO x co-loaded TiO2 catalysts for low-temperature CO2 hydrogenation to form CH3OH
Groß Reactivity of bimetallic systems studied from first principles
Marcinkowski et al. Selective formic acid dehydrogenation on Pt-Cu single-atom alloys
EP2069283B1 (en) Method for the production of aromatic amines in a fluidized bed reactor
CN100379710C (en) Paraffin alkylation
CA2027512C (en) Process and structure for effecting catalytic reactions in distillation structure
CA2493811A1 (en) Contact structures
US20050014635A1 (en) Supported catalysts having a controlled coordination structure and methods for preparing such catalysts
Chang et al. Rational design of single-atom-doped Ga2O3 catalysts for propane dehydrogenation: breaking through volcano plot by Lewis acid–base interactions
EP1715946A1 (en) Reactor and method for producing chlorine from hcl
US5523062A (en) Catalytic distillation distribution structure
WO2019020705A1 (en) Catalytic reactor comprising fibrous catalyst particles support
US3875055A (en) Apparatus and method
CN207041947U (en) A kind of catalytic distillation module
EP3658268A1 (en) Catalytic reactor comprising fibrous catalyst particles support
US20030106837A1 (en) Heterogeneously catalyzed reactions and apparatus therefor
CN114471377B (en) Reactor and reaction method for removing olefin from reforming generated oil
CN1286558C (en) Catalyst filling material for selective hydrogenation
JP2965373B2 (en) Method for improving octane number and increasing the amount of light reformate from catalytic reformer
EP2066583B1 (en) Method for producing chlorine in a fluidized bed reactor
CN1602988A (en) Catalyst distillation component and catalyst distillation method used said component
TH57807B (en) Tactile structure
TH66064A (en) Tactile structure
CN219580511U (en) Tubular fixed bed reactor

Legal Events

Date Code Title Description
EEER Examination request
MKLA Lapsed

Effective date: 20210726